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Publication numberUS4267062 A
Publication typeGrant
Application numberUS 06/042,885
Publication dateMay 12, 1981
Filing dateMay 29, 1979
Priority dateOct 21, 1977
Publication number042885, 06042885, US 4267062 A, US 4267062A, US-A-4267062, US4267062 A, US4267062A
InventorsThomas L. Byerley
Original AssigneeNl Industries, Inc.
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Abandoned borehole compositions
US 4267062 A
Abstract
Compositions for boreholes which are to become abandoned and to a process for using the same wherein the compositions contain a mixture of about 89.5% to about 99.4% by weight clay gellant, about 0.5% to about 10% by weight water-soluble alkali metal salt, and about 0.1% to about 3.0% by weight salt of carboxymethylcellulose.
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Claims(3)
What is claimed is:
1. A process for suspending solids and controlling formation pressures within a borehole to be abandoned which comprises:
(a) preparing a composition essentially comprising about 89.5 to about 99.4% by weight water swellable clay gellant selected from the group consisting of natural and synthetic, sodium form montmorillionite, bentonite, beidellite, hectorite, saponite, stevensite, and mixtures thereof, about 0.5% to about 10% by weight water-soluble alkali metal salt selected from the group consisting of sodium and potassium carbonates, bicarbonates, citrates, oxalates, stearates, and mixtures thereof and about 0.1 to about 3.0% by weight of a water soluble, essentially non-hygroscopic salt of carboxymethylcellulose, having a degree of substitution in the range of about 0.5 to 1.5, selected from the group consisting of sodium carboxymethylcellulose, potassium carboxymethylcellulose and mixtures thereof;
(b) Mixing said composition of step (a) with fresh water to form an aqueous slurry having a gel strength of at least 20 lb/100 ft2 and having an API filtration rate less than about 15 cc/30 minutes;
(c) Circulating said aqueous slurry throughout the total depth of said borehole and allowing said aqueous slurry to remain in the borehole.
2. The process of claim 1 wherein said composition comprises about 92 to about 97.5 by weight sodium bentonite, about 2 to about 6% by weight of said water soluble alkali metal salt, and about 0.5 to 2% by weight of said salt of carboxymethylcellulose, and wherein said composition comprises about 1 to about 30 lb/bbl of said aqueous slurry.
3. The process of claim 1 wherein the aqueous slurry API funnel viscosity is raised by at least 20 seconds/quart.
Description

This is a continuation of application Ser. No. 844,279, filed Oct. 21, 1977, now abandoned.

This invention relates to compositions for boreholes which are to become abandoned and to a process for using the same.

When relatively shallow wells are drilled with rotary drilling equipment such as in water and gas exploration, mineral exploration, and seismic hole testing, a drilling fluid is generally circulated down the drill pipe to the bit and back up the hole to the surface. The drilling fluid performs many functions which are vital to the success of the drilling process. Generally, the best drilling fluids are aqueous suspensions of suspended solids, such as clay which readily form colloidal dispersions that are stable and low in viscosity.

Upon completion of the drilling process and of the desired exploration or testing procedures, the boreholes have generally been abandoned without any additional treatment to seal the hole. Abandoned boreholes containing the aforementioned drilling fluids, however, have not maintained a stabilized condition. For example, loss of mud to the surrounding formation in exploratory boreholes in New Mexico, U.S.A. have been repeatedly observed with corresponding decreases in filtration control and fluid gel strength.

Environmental regulations have been recently adopted which attempt to prevent continuation of these practices. One such regulation has been passed in New Mexico which regulation requires an abandoned borehole to contain a mud system that will maintain a high viscosity while decreasing fluid loss from the borehole over extended periods of time in order to obtain the necessary filtration control and gel strength to suspend solids and control formation pressures.

The present invention provides a composition for use in boreholes being abandoned, which composition when used in an aqueous fluid, such as water or an aqueous drilling mud system increases the viscosity of the fluid while it decreases fluid loss after placement throughout the total depth of the borehole.

The borehole additive compositions of this invention comprise a mixture of about 89.5% to about 99.4% by weight clay gellant, about 0.5% to about 10% by weight water-soluble alkali metal salt, and about 0.1% to about 3.0% by weight salt of carboxymethylcellulose.

The borehole additive compositions of this invention are used by adding a sufficient amount of the composition with mixing to an aqueous fluid until the fluids funnel viscosity is raised by at least 10 seconds/quart, and preferably 20 seconds/quart, and passing the treated fluid into the borehole.

The compositions are used in sufficient amounts to prepare a colloidal suspension with low unit weight and with suitable viscosity, good gel properties and low filtrate loss. These desirable properties are achieved when the compositions are added to fresh water to prepare a viscous suspension or when added to increase the viscosity of an aqueous mud system already in use in amounts to increase the API funnel viscosity by at least 10 seconds/quart and preferably by at least 20 seconds/quart. It has been found that the necessary API funnel viscosity can be achieved by employing about 1 lb/bbl to 30 lb/bbl (42 gallon barrel) of the composition in the aqueous system. The exact amount added, however, may vary depending on water hardness and existing mud system properties. Besides increasing funnel viscosity, the resulting aqueous systems will have a minimum ten minute gel strength of 20 lb/100 sq. ft. and a maximum API filtrate of 15.0 cc/30 min, and preferably 10.0 cc/30 min.

The clays used to prepare the compositions of this invention are smectite-type clays which have a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay. Particularly desirable types of clay are the naturally-occurring Wyoming varieties of swelling bentonites and like clays, and hectorite, a swelling magnesium-lithium silicate clay.

The clays, especially the bentonite type clays, are preferably converted to the sodium form if they are not already in this form. This can conveniently be done by preparing an aqueous clay slurry and passing the slurry through a bed of cation exchange resin in the sodium form. Alternatively, the clay can be mixed with water and a soluble sodium compound such as sodium carbonate, sodium hydroxide and the like and shearing the mixture with a pugmill or extruder.

Smectite-type clays prepared synthetically by either a pneumatolytic or, preferably a hydrothermal synthesis process can also be used. Representative of such clays are montmorillonite, bentonite, beidellite, hectorite, saponite and stevensite. These clays may be synthesized hydrothermally by forming an aqueous reaction mixture in the form of a slurry containing mixed hydrous oxides or hydroxides of the desired metals with or without sodium flouride or alternate exchangeable cation of mixture thereof in the proportions for the particular synthetic smectite desired. The slurry is then placed in an autoclave and heated under autogenous pressure to a temperature within the range of approximately 100 to 325 C., preferably 274 to 300 C., for a sufficient period of time to form the desired product. Representative hydrothermal processes for preparing synthetic smectites are described in the following United States patents, incorporated herein by reference; U.S. Pat. Nos. 3,252,757 to Granquist; 3,586,478 to Neumann; 3,666,407 to Orlemann; 3,671,190 to Neumann; 3,844,978 and 3,844,979 to Hickson; and 3,852,405 and 3,855,147 to Granquist.

The clay gellants are employed in amounts of about 89.5 to about 99.4% by weight and preferably about 92.0 to about 97.5% by weight of the composition. These amounts of clay gellant are necessary to achieve the requisite gel strengths and funnel viscosities.

The water-soluble alkali metal salts used in the compositions of this invention may be selected from a wide range of materials, both inorganic and organic, which are reactive with calcium and magnesium salts and other hardness causing salts to form insoluble compounds. Calcium salts, such as anhydrite or gypsum, seriously impair the suspending and sealing properties of the clay gellant.

The water-soluble alkali metal salts are employed in amounts of about 0.5 to about 10% by weight, and preferably about 2 to about 6% by weight of the composition. It has been found that these amounts are sufficient to remove the cations normally present in the solution. Amounts less than 0.5% are not effective in curbing the adverse effects of the hardness cations. Amounts greater than 10% should not be employed since these high amounts may begin to flocculate the clay gellant with resulting loss in filtration control. The water-soluble alkali metal salts useful in the invention are described in U.S. Pat. No. 2,433,668 and are preferably selected from sodium carbonate, potassium carbonate, sodium bicarbonate, potassium bicarbonate, sodium citrate, potassium citrate, sodium oxalate, potassium oxalate, sodium stearate and potassium stearate.

The salts of carboxymethylcellulose used in the composition of this invention are preferably selected from potassium and sodium. These materials should be (a) readily soluble in water or alkali solutions; (b) neutral or alkaline in solution; (c) non-hygroscopic or essentially non-hygroscopic (d) low in transition metal content, and (e) have a preferred degree of substitution from 0.5 to 1.5 and most preferably from 0.6 to 0.8.

The carboxymethylcellulose is added in sufficient amounts to decrease the fluid filtration rate and cake thickness, yet promote hole stability in water-sensitive formations. These properties have been achieved when amounts of about 0.1 to about 3.0% by weight, preferably about 0.5 to about 2.0% by weight material is employed in the composition. Amounts less than 0.1% do not provide sufficient yield point and gel strengths. Amounts higher than 3.0%, while maintaining filtration control are not able to maintain a controlled flocculation of the clay gellant.

The compositions of this invention are prepared by conventional dry mixing procedures. The method of addition is not critical. It is advisable, however, to obtain a homogenous mixture of the ingredients prior to their dispersal in the aqueous fluid. The aqueous fluid may be water, or an aqueous mud system, such as a drilling fluid already in use.

Dispersion is easily accomplished by carrying out mixing in a fluid mud mixer, hopper or other conventional device. The composition may optionally be dispersed in water prior to mixing with an aqueous mud system. Once dispersed, the compositions are circulated throughout the total depth of the borehole. Once circulation is complete, the fluid is allowed to remain in the borehole without additional treatment and the borehole abandoned, providing the necessary increase in funnel viscosity has been achieved. The ability to obtain and maintain fluid viscosities with low filtrate loss in fluids used in abandoned boreholes has heretofore not been achieved to the level obtained by use of the inventive compositions.

The following examples are given to illustrate the invention but are not deemed to be limiting thereof. All percentages given are based upon weight unless otherwise indicated. All measurements were performed in accordance with the American Petroleum Institutes Standard Procedure for Testing Drilling Fluids identified as API RP13B, 6th Ed., April, 1976.

EXAMPLE 1 Runs 1 to 7

An additive for a borehole being abandoned was prepared by mixing 95% Wyoming bentonite, 4% sodium carbonate and 1% sodium carboxymethylcellulose, all percentages are by weight. This composition was used to treat various drilling fluids used in drilling mineral exploratory boreholes. The results are set forth in Table 1. The drilling fluids and water in Runs 1 to 4 were from the Churchrock area of New Mexico. The drilling fluids and water in Runs 5 and 6 were from the Ambrosia Lake area of New Mexico, whereas the drilling fluid in Run 7 was from the Nose Creek area of New Mexico.

The data indicates that fluids prepared with the inventive compositions will have commercially effective minimum ten minute gel strengths and maximum API filtrates for use as borehole abandonment fluids. The blanks in the table represent those values which were not measured.

                                  TABLE 1__________________________________________________________________________                                Nose                        Ambrosia                                Creek         Churchrock Area                        Lake Area                                AreaSample No.    1   2   3   4  5   6   7__________________________________________________________________________Initial DataWeight (ppg)  10.2             10.1                 10.4                     8.33                        9.4 8.33                                9.5Funnel Viscosity (sec/qt)         38  38  44  26 30  26  31.5Plastic Viscosity (cp)         15  13  20  0  6   0   6Yield Point (lb/100 sq ft)         15  4   5   0  2   0   1Gel Strength (lb/100 sq ft)-         7/17             7/15                 7/15                     0/0                        2/5 0/0 0/010 sec/10 minFiltrate, API (ml/30 min)         15.2             13.0                 10.4                     -- 42.0                            --  4Total Hardness (ppm)         32  48  32  -- 248 400 48Sand Content (% by Vol.)         5   5   5   -- 2   --  .2Solids Content (% by Vol.)         13.5             12.2                 15  -- 7.7 --  --Water Content (% by Vol.)         86.5             87.8                 85  100                        92.3                            100 --Additivelb/bbl.       3.2 4.0 3.0 20.0                        7.6*                            20.0                                12Final DataFunnel Viscosity (sec/qt)         48  48  60  38 80  39  59Plastic Viscosity (cp)         17  18  23  6  22  9   23Yield Point (lb/100 sq ft)         14  14  17  10 21  12  11Gel Strength (lb/100 sq ft)-         10/23             12/24                 10/26                     8/25                        17/38                            12/24                                11/2310 sec/10 minFiltrate, API (ml/30 min)         10.4             7.8 6.4 10.4                        8.8 11.2                                8.4Total Hardness (ppm)         28  40  32  -- 140 --  60__________________________________________________________________________ *This additive contained 93.75% Wyoming bentonite, 4.61% sodium carbonate and 1.64% CMC.
EXAMPLE 2 Runs 8 to 11

Compositions were prepared containing various concentrations of Wyoming bentonite, sodium carbonate and sodium carboxymethylcellulose. The samples were added in amounts of 20 lb/bbl (42 gallon barrel) to deionized water which had been saturated with gypsum and mixed for 20 minutes. The results are set forth in Table II.

The invention being thus described, it will be obvious that the same may be varied in many ways. Such variations are not to be regarded as a departure from the spirit and scope of the invention, and all such modifications are intended to be included within the scope of the following claims.

              TABLE II______________________________________         Run 8 Run 9   Run 10  Run 11______________________________________Additive compositionWyoming Bentonite           95      96      97    98Sodium Carbonate           4       3       2     1CMC             1       1       1     1Treated FluidPlastic Viscosity, (cp)           9       8       5.5   3Yield Point (lb./100 sq ft)           16      13      10    6Gel Strength (lb./100 sq ft)           20/50   17/44   10/32 5/1210 sec/10 minFiltrate, API (ml/30 min.)           8.6     8.5     9.4   12.5______________________________________
Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2425768 *Aug 12, 1944Aug 19, 1947Phillips Petroleum CoDrilling fluids and method of use
US2776259 *Sep 28, 1955Jan 1, 1957Exxon Research Engineering CoDrilling muds
US3081260 *Mar 25, 1960Mar 12, 1963Pan American Petroleum CorpLow solids drilling fluid
US3380522 *Jun 8, 1965Apr 30, 1968Marion Dudley HughesMethod of inhibiting saline water intrusion into fresh water aquifers
AU140931A * Title not available
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Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US4441556 *Aug 17, 1981Apr 10, 1984Standard Oil CompanyDiverter tool and its use
US4655842 *Aug 12, 1985Apr 7, 1987W. R. Grace & Co.Citrate swelling agents
US4780147 *Mar 19, 1987Oct 25, 1988W. R. Grace & Co.Vermiculite dispersions and method of preparing same
US4888120 *Sep 9, 1987Dec 19, 1989Henkel Kommanditgesellschaft Auf AktienWater-based drilling and well-servicing fluids with swellable, synthetic layer silicates
US5102464 *Oct 31, 1990Apr 7, 1992W. R. Grace & Co.-Conn.Swelling and delamination by treating with anionic chelating agent
US5266538 *Dec 21, 1990Nov 30, 1993Southern Clay Products, Inc.Group 1A salt, swelling and gelation inhibition
US5391228 *May 1, 1992Feb 21, 1995Southern Clay Products, Inc.Method for preparing high solids bentonite slurries
US5723416 *Apr 1, 1997Mar 3, 1998Liao; W. AndrewWell servicing fluid for trenchless directional drilling
US6009946 *Nov 14, 1997Jan 4, 2000Exploration Products Company, LlcDevice for sealing charges in shot holes and a method for using the same
US6667279Nov 13, 1997Dec 23, 2003Wallace, Inc.Swellable polymer gel for wells; crosslinking system is either a redox system or a chelating system
US8205674Jul 24, 2007Jun 26, 2012Mountain West Energy Inc.Apparatus, system, and method for in-situ extraction of hydrocarbons
DE3631764A1 *Sep 18, 1986Mar 24, 1988Henkel KgaaVerwendung von quellfaehigen, synthetischen schichtsilikaten in waessrigen bohrspuel- und bohrlochbehandlungsmitteln
EP0260538A2Sep 3, 1987Mar 23, 1988Henkel Kommanditgesellschaft auf AktienUse of expandable synthetic lamellar silicates in aqueous drilling or borehole treatment fluids
WO1993008230A1 *Oct 19, 1992Apr 29, 1993Laporte Industries LtdCellulose ether thickening compositions
WO1998044070A1 *Mar 31, 1998Oct 8, 1998Dresser IndWell servicing fluid for trenchless directional drilling
Classifications
U.S. Classification507/215, 166/305.1
International ClassificationE21B33/00, C09K8/16, C09K8/14
Cooperative ClassificationC09K8/145, C09K8/16, E21B33/00
European ClassificationC09K8/14B, E21B33/00, C09K8/16
Legal Events
DateCodeEventDescription
May 7, 1992ASAssignment
Owner name: BAROID CORPORATION, TEXAS
Free format text: RELEASED BY SECURED PARTY;ASSIGNOR:CHASE MANHATTAN BANK, THE;REEL/FRAME:006085/0590
Effective date: 19911021
Mar 8, 1989ASAssignment
Owner name: CHASE MANHATTAN BANK (NATIONAL ASSOCIATION), THE
Free format text: SECURITY INTEREST;ASSIGNOR:BAROID CORPORATION, A CORP. OF DE.;REEL/FRAME:005196/0501
Effective date: 19881222
Feb 14, 1988ASAssignment
Owner name: BAROID TECHNOLOGY, INC., DELAWARE
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:NL INDUSTRIES, INC., A NJ CORP.;REEL/FRAME:005091/0020
Effective date: 19890210